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V2O5-WO3/TiO2催化氧化NO性能研究

atalytic oxidation of NO over V2O5-WO3/TiO2 catalyst and the effct of H2O and SO2 on NO conversion

中文摘要英文摘要

采用浸渍法制备了催化剂V2O5-WO3/TiO2,考察了组分配比、焙烧温度等制备条件和反应温度、NO进口体积分数、O2含量、空速等操作条件对催化氧化NO活性的影响,研究了其对抗H2O、SO2毒化的能力。对载体和催化剂分别进行了BET、XRD和FT-IR分析,结果表明,在最佳条件下制备的催化剂,在反应温度120℃、NO体积分数550×10-6、O2体积分数10%、空速5000 h-1条件下,NO转化率可以达到31.2%,此时与湿法吸收装置串联可以取得高于70%的脱硝效率,能够满足NOx浓度低于1100 mg/m3的吸收要求。催化剂在反应温度为120℃时缓慢中毒,但在加热到250℃后活性基本可以恢复,因此可以采用双床并联的操作模式,一个进行催化氧化反应另一个进行加热再生,可有效应用于烟气NOx的氧化吸收。

V2O5-WO3/TiO2 catalyst was prepared by impregnation method. The effects of loading, calcining temperature, volume fractions of NO and O2, and space velocity on V2O5-WO3/TiO2 catalytic oxidation of nitric oxide were studied, and the resistance to poisoning of H2O and SO2 was investigated. The support and catalysts were characterized by BET, XRD and FT-IR analysis. The results showed that the optimum catalyst can obtain the oxidation rate about 31.2%, when the volume fraction of NO 550×10-6, O2 10% and space velocity 5000 h-1 at 120℃, at this point in series with the wet absorbing device can be made higher than the 70% denitrification efficiency, could meet the NOx concentrations of less than 1100 mg/m3 absorption requirements. The catalyst's poisoning is slow at 120℃, but activity can be restored after heated to 250℃, so we can use twin-bed parallel mode of operation, one bed for catalytic oxidation reaction and the other for heating regeneration, this mode can be applied to oxidative absorption NOx of flue gas effectively.

秦旭东、王娇、张俊丰、颜斌

环境污染、环境污染防治化学无机化学工业

催化氧化H2OSO2NO

catalytic oxidationH2OSO2NO

秦旭东,王娇,张俊丰,颜斌.V2O5-WO3/TiO2催化氧化NO性能研究[EB/OL].(2010-09-28)[2025-08-05].http://www.paper.edu.cn/releasepaper/content/201009-615.点此复制

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